Process for producing 17-acetals of 3-alkoxyestra-2,5(10)-dien-17-ones

ABSTRACT

17-Acetals of 3-alkoxyestra-2,5(10)-dien-17-ones are prepared by reacting 17-acetals of 3-alkoxyestra-1,3-5(10)-trien-17-ones with sodium or potassium, liquid ammonia and a tertiary alcohol in the presence of a solvent selected from the group consisting of tetrahydrofuran, dioxane and tetrahydropyran. 
     Yield and selectivity of this reaction are improved by using the 17-acetals of the 3-alkoxyestra-1,3,5(10)-trien-17-ones, sodium or potassium, liquid ammonia and the solvent in such proportions that the 17-acetals of the 3-alkoxyestra-1,3,5(10)-trien-17-ones are substantially dissolved in the reaction system and that two liquid phases are formed, the lower phase being colored.

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention relates to a process for producing 17-acetals of 3-alkoxyestra-2,5(10)-dien-17-ones. More particularly, this invention relates to a commercially practical process for producing 17-acetals of 3-alkoxyestra-2,5(10)-dien-17-ones by Birch reduction of 17-acetals of 3-alkoxyestra-1,3,5(10)-trien-17-ones.

The 17-acetals of the 3-alkoxyestra-2,5(10)-dien-17-ones are useful as intermediates in the preparation of steroidal hormones such as 19-norethisterone.

2. Description of the Prior Art

Japanese Published Patent 17,030/1960 discloses a process for producing 3-methoxyestra-2,5(10)-dien-17-one ethylene acetal, which comprises reacting 3-methoxyestra-1,3,5(10)-trien-17-one ethylene acetal with lithium or sodium, liquid ammonia and isopropanol in the presence of ethyl ether. This process has the disadvantage of using larger amounts of ethyl ether and liquid ammonia.

It is known that a 1,4-dihydrosteroid e.g., 3-methoxyestra-2,5(10)-dien-17-one diethyl acetal, is produced by reacting an aromatic steroid, e.g., 3-methoxyestra-1,3,5(10)-trien-17-one diethyl acetal with lithium or sodium, liquid ammonia and tert-butanol in the presence of tetrahydrofuran. (See Organic Reactions in Steroid Chemistry edited by John Fried and John A. Edwards, Van Nostrand Reinhold Company, in volume 1 at pages 25-27 and 49-50, and J. Org. Chem., 26 3237-3245 (1961)).

A disadvantage of this process is that the use of larger amounts of tert-butanol serving as a proton donor as well as a solvent results in lower reaction rates.

It is therefore an object of this invention to provide a process that is capable of producing 17-acetals of 3-alkoxyestra-2,5(10)-dien-17-ones from 17-acetals of 3-alkoxyestra-1,3,5(10)-trien-17-ones in high yield and selectivity. It is another object to produce 17-acetals of 3-alkoxyestra-2,5(10)-dien-17-ones by a process which does not suffer from the disadvantages associated with processes employing larger volumes of a solvent, e.g., ethyl ether, tert-butanol, and liquid ammonia.

Still another object of this invention is to provide a commercially practicable process for producing 17-acetals of 3-alkoxyestra-2,5(10)-dien-17-ones which permits reliable and reproducible manufacturing operation. These and other objects are accomplished by the invention described herein.

SUMMARY OF THE INVENTION

Briefly stated, this invention is a process for producing 17-acetals of 3-alkoxyestra-2,5(10)-dien-17-ones by the Birch reduction of 17-acetals of 3-alkoxyestra-1,3,5(10)-trien-17-ones which comprises using not more than 90 ml (measured at a boiling point of the reaction system) of liquid ammonia per gram of sodium or potassium, not more than 100 ml (measured at 15° C) of tetrahydrofuran, dioxane or tetrahydropyran per gram of sodium or potassium, sodium or potassium, and a 17-acetal of a 3-alkoxyestra-1,3,5(10)-trien-17-one in such proportions that the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one is substantially dissolved in the reaction system and that two liquid phases are formed in the reaction system, the upper phase consisting mainly of sodium or potassium, and liquid ammonia, and the colored lower phase consisting mainly of tetrahydrofuran, dioxane or tetrahydropyran, liquid ammonia and the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one.

DETAILED DESCRIPTION OF THE INVENTION

The reaction embraced by the process of this invention is illustrated by the following reaction scheme: ##STR1## In accordance with the process of this invention, the 17-acetal of the 3-alkoxyestra-2,5(10)-dien-17-one (I) (hereinafter referred to as ESD) is obtained by the Birch reduction of the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one (II) (hereinafter referred to as ETA).

In the above-described formulas (I) and (II), R₁ and R₂ when considered separately are alkyl of 1-10 (preferably 1-5) carbon atoms such as methyl, ethyl, propyl, butyl or the like; R₁ and R₂ when taken together are alkylene of 2-10 (preferably 2-5) carbon atoms such as ethylene, propylene, trimethylene, tetramethylene or the like; and R₃ is alkyl of 1-10 (preferably 1-5) carbon atoms such as methyl, ethyl, propyl, butyl or the like.

Representative of ETA which is used in the process of this invention are:

3-methoxyestra-1,3,5(10)-trien-17-one ethylene acetal

3-ethoxyestra-1,3,5(10)-trien-17-one ethylene acetal

3-methoxyestra-1,3,5(10)-trien-17-one dimethyl acetal

3-methoxyestra-1,3,5(10)-trien-17-one diethyl acetal

3-ethoxyestra-1,3,5(10)-trien-17-one diethyl acetal

3-methoxyestra-1,3,5(10)-trien-17-one propylene acetal

3-methoxyestra-1,3,5(10)-trien-17-one tetramethylene acetal

Especially preferred is 3-methoxyestra- 1,3,5(10)-trien-17-one ethylene acetal.

In accordance with the process of this invention, the Birch reduction of ETA is effected using sodium or potassium (preferably sodium) as the reducing agent; a tertiary alcohol e.g., tert-butyl alcohol, tert-amyl alcohol (preferably tert-butyl alcohol) as the proton donor; liquid ammonia; and the solvent which is tetrahydrofuran, dioxane or tetrahydropyran (preferably tetrahydrofuran).

Sodium or potassium is used as a reducing agent. However, the use of potassium on a commercial scale is dangerous because of the vigorous reaction of potassium with water. Therefore, sodium is the preferred reducing agent.

It is not preferred to use lithium instead of sodium or potassium because of the low selectivity and the difficulty in controlling the reaction on a commercial scale associated with a higher reaction rate.

The preferred tertiary alcohols are tert-butyl alcohol and tert-amyl alcohol which give the high selectivity. Especially preferred is tert-butyl alcohol.

The presence of a solvent which dissolves ETA into the reaction system is required because of the slight solubility of ETA in liquid ammonia. Such solvents include tetrahydrofuran, dioxane and tetrahydropyran which readily dissolve ETA. The preferred solvent is tetrahydrofuran because of its low boiling point.

In the process of this invention, a combination of sodium, liquid ammonia and tetrahydrofuran will give the best results.

Characteristic features of the process of this invention are the amounts of sodium or potassium, liquid ammonium, the solvent and ETA to be used, and the proportions thereof. Criticality of the amounts of the four components to be used and the proportions thereof will be more fully explained in conjunction with the attached drawing which illustrates a change of a phase state with the amounts of liquid ammonia, tetrahydrofuran and 3-methoxyestra-1,3,5(10 )-trien-17-one ethylene acetal (hereinafter referred to EMK) or sodium to be used. In the drawing, the X axis represents the amount (ml) of liquid ammonia to be used, which is measured at the boiling point of the system, and the Y axis represents the amount (ml) of tetrahydrofuran to be used, which is measured at 15° C. When the amounts of liquid ammonia and tetrahydrofuran to be used per gram of sodium are in the region above Line A of the drawing, two liquid phases are formed, the upper phase being reddish-copper colored and consisting mainly of sodium and liquid ammonia, and the lower phase consisting mainly of tetrahydrofuran, liquid ammonia and EMK. When they are in the region below Line A of the drawing, a single phase having a reddish-copper to deep blue color is formed.

When they are in the region above Line C of the drawing, the lower phase consisting mainly of tetrahydrofuran, liquid ammonia and EMK is substantially colorless. When they are in the region below Line C of the drawing, the lower phase is deep blue.

When the lower phase consisting mainly of tetrahydrofuran, liquid ammonia and EMK is colorless, sodium is not dissolved in the lower phase. On the other hand, when the lower phase is colored, sodium is dissolved in the lower phase.

When the amounts of liquid ammonia and tetrahydrofuran to be used per gram of EMK are in the region above Line B of the drawing, EMK is completely dissolved in the system. When they are in the region below Line B of the drawing, EMK is not completely dissolved in the system.

In order to increase the rate of reaction, it is essential that EMK be substantially dissolved in the reaction system. When a portion of EMK is present in the form of a solid, the rate of reaction is very low. In order to further increase the rate of reaction, it is essential that sodium be dissolved in the lower phase in which EMK is substantially dissolved.

When sodium is not substantially dissolved in the lower phase in which EMK is substantially dissolved, good contact of the upper and lower phases will be required by means of vigorous stirring which is not economically advantageous.

Therefore, it is preferred that the amounts of liquid ammonia and tetrahydrofuran to be used per gram of sodium be in the region below Line C, and that the amounts of liquid ammonia and tetrahydrofuran to be used per gram of EMK be in the region above Line B.

When the amounts of liquid ammonia and tetrahydrofuran to be used per gram of sodium are in the region below Line A, EMK, in many cases, is not completely dissolved in the reaction system. This fact will be explained by slight amounts of liquid ammonia and tetrahydrofuran to be used and by the ratio of sodium to EMK, which will be described below.

As apparent from the above, in order to increase the rate of the Birch reduction, it is essential that ETA be substantially dissolved in the reaction system, and that a reducing agent sodium or potassium be dissolved in the lower phase in which ETA is substantially dissolved. However, in order for the process of this invention to be economically attractive, it is not preferred to use larger amounts of liquid ammonia and the solvent.

The amount of liquid ammonia to be used per gram of sodium or potassium is generally not more than 90 ml, preferably not more than 75 ml and more preferably 60 ml, each being measured at the boiling point of the system.

The amount of the solvent to be used per gram of sodium or potassium is generally not more than 100 ml, preferably not more than 75 ml and more preferably not more than 60 ml, each being measured at 15° C.

In a preferred embodiment of the process of this invention, which is a combination of sodium, EMK, tetrahydrofuran and liquid ammonia, sodium : EMK : tetrahydrofuran: liquid ammonia is 1g : 0.5-4.0 g : 25-100 ml : 25-90 ml and preferably 1 g : 1.0-2.5 g : 30-70 ml : 35-70 ml, provided that EMK is substantially dissolved in the reaction system and that two liquid phases are formed, the lower phase being colored. At least 2 gram equivalents of sodium or potassium is used per mole of ETA.

The preferred amount of sodium or potassium to be used is in the range of 3.0 to 10 gram equivalents of sodium or potassium per mole of ETA.

A tertiary alcohol is added in an amount sufficient to give 2 equivalents of proton per mole of ETA. In the process of this invention, the tertiary alcohol serves substantially as a proton donor.

Increasing the amount of the tertiary alcohol to be used decreases the solubility of sodium or potassium as well as the rate of the Birch reduction, because sodium or potassium is exhausted promptly by the reaction between sodium or potassium, and the tertiary alcohol. Therefore, it is preferred to add the tertiary alcohol in an amount to give 2 to 4 equivalents of proton per mole of ETA.

In general, the tertiary alcohol is added 0.5 to 2 hours after the initiation of the reaction.

In contrast to the prior art processes which suffer the drawbacks, such as, low yield and selectivity, and low level of reliability and reproducibility, the process of this invention makes it possible to produce ESD in high yield and selectivity, and with high level of reliability and reproducibility which is essential and suitable in a commercial scale operation.

An additional advantage of the process of this invention is efficiency and economy associated with the use of smaller amounts of the solvent and liquid ammonia.

BRIEF DESCRIPTION OF THE DRAWING

The drawing illustrates a change of a phase state with the amounts of liquid ammonia, tetrahydrofuran and EMK or sodium to be used.

In the drawing, the X axis represents the amount (ml) of liquid ammonia to be used, which is measured at a boiling point of the system, and the Y axis represents the amount (ml) of tetrahydrofuran to be used, which is measured at 15° C. When the amounts of liquid ammonia and tetrahydrofuran to be used per gram of sodium are in the region above Line A of the drawing, two liquid phases are formed, the upper phase being reddish-copper colored and consisting mainly of sodium and liquid ammonia, and the lower phase consisting mainly of tetrahydrofuran, liquid ammonia and EMK. When they are in the region below Line A of the drawing, a single phase having a reddish-copper to deep blue color is formed.

When they are in the region above Line C of the drawing, the lower phase consisting mainly of tetrahydrofuran, liquid ammonia and EMK is colorless. When they are in the region below Line C of the drawing, the lower phase is deep blue.

When the amounts of liquid ammonia and tetrahydrofuran to be used per gram of EMK are in the region above Line B of the drawing, EMK is completely dissolved in the system. When they are in the region below Line B of the drawing, EMK is not completely dissolved in the system.

EXAMPLES

The following examples are presented to further illustrate this invention but are not intended to limit the scope thereof. Unless otherwise stated, all percents are on a molar basis. As used in the description of the examples, the following terms have the following meanings: conversion means a mole of (EMK reacting -- EMK remaining) per mole of EMK reacting, generally expressed as a percentage, selectivity means a mole of 3-methoxyestra-2,5(10)-dien-17-one 17-ethylene acetal (hereinafter referred to MEE) which is formed per mole of EMK reacting, generally expressed as a percentage.

EXAMPLE 1

A 100 ml., three-necked round bottom glass flask, fitted with an ammonia gas inlet tube, a Dry Ice cooled condenser and an agitator is charged with 1.0 g of EMK, 0.5 g of sodium and 25 ml of tetrahydrofuran EMK is dissolved with stirring. A 30-ml portion of liquid ammonia, after being vaporized, is introduced to the flask and then the temperature of the reaction mixture falls to - 28° to -29° C. At the end of this period, the reaction mixture separates into two liquid phases, the reddish-copper colored upper phase consisting mainly of liquid ammonia and sodium, and the deep blue lower phase consisting mainly of EMK, tetrahydrofuran, liquid ammonia and a small amount of sodium. After the reaction mixture is stirred at about 200 rpm for one hour, a mixture of 1 ml of tetrahydrofuran and 2 ml of tert-butanol is added to the flask over a period of 5 minutes. Stirring is continued for 2 hours. At the end of this period, the reddish-copper colored upper phase almost disappears and a nearly single phase having a deep blue color is formed.

After liquid ammonia is removed by distillation in a water bath, tetrahydrofuran is removed by distillation in vacuo at a temperature below 30° C to yield a crystalline solid which is extracted with 15 ml of benzene. The benzene layer is washed with water, dried, removed by distillation in vacuo at a temperature below 40° C and then dried to give 1.0 g of crude MEE.

Gas chromatographic analysis indicated a 99.7% conversion and a 92.5% selectivity.

EXAMPLE 2

Using 1.0 g of EMK, 0.5 g of sodium, 40 ml of tetrahydrofuran and 40 ml of liquid ammonia, Example 1 is repeated to give 1.0 g of crude MEE.

Gas chromatographic analysis indicated a 99.6% conversion and a 92.5% selectivity.

EXAMPLE 3

Using 1.0 g of EMK, 0.5 g of sodium, 30 ml of tetrahydrofuran and 35 ml of liquid ammonia, Example 1 is repeated to give 1.0 g of crude MEE.

Gas chromatographic analysis indicated a 99.9% conversion and a 92.7% selectivity.

EXAMPLE 4

Using 1.0 g of EMK, 0.7 g of sodium, 28 ml of tetrahydrofuran and 35 ml of liquid ammonia, Example 1 is repeated to give 1.0 g of crude MEE.

Gas chromatographic analysis indicated a 99.9% conversion and a 92.0% selectivity.

REFERENCE EXAMPLE 1

This reference example illustrates that when EMK is not completely dissolved in the reaction system, the conversion is low.

Using 1.0 g of EMK, 0.5 g of sodium, 20 ml of tetrahydrofuran and 30 ml of liquid ammonia, Example 1 is repeated. When liquid ammonia is introduced, a portion of EMK which has been dissolved precipitates.

Yield of crude MEE is 1 g.

Gas chromatographic analysis indicated a 83.2% conversion and a 93.3% selectivity.

REFERENCE EXAMPLE 2

This reference example illustrates that although EMK is not dissolved, prolongation of the reaction time increases the conversion. Reference Example 1 is repeated except that the reaction time after the addition of tert-butanol is 8 hours.

Yield of crude MEE is 1 g.

Gas chromatographic analysis indicated a 99.3% conversion and a 93.1% selectivity.

REFERENCE EXAMPLE 3

Using 1.0 g of EMK, 1.0 g of sodium, 10 ml of tetrahydrofuran and 40 ml of liquid ammonia, Example 1 is repeated. The reaction mixture does not separate into the two liquid phases and becomes deep brown. This state is held until the reaction is terminated.

Gas chromatographic analysis indicated a 86.4% conversion and a 90.7% selectivity.

REFERENCE EXAMPLE 4

Reference Example 3 is repeated except that the reaction time after the addition of tert-butanol is 8 hours.

Yield of crude MEE is 1.0 g.

Gas chromatographic analysis indicated a 89.8% conversion and a 88.5% selectivity.

REFERENCE EXAMPLE 5

This reference example illustrates that when EMK is dissolved and sodium is scarcely dissolved in the lower phase, intensification of the stirring increases the conversion. A 200 ml., three-necked round bottom glass flask, fitted with an ammonia gas inlet tube, a Dry Ice cooled condensor and an agitator is charged with 1.0 g of EMK, 1.0 g of sodium, 50 ml of tetrahydrofuran and 30 ml of liquid ammonia. The reaction mixture is separated into two liquid phases, the upper phase being reddish-copper colored and the lower phase being colorless. After the reaction mixture is stirred at about 600 rpm for one hour, a mixture of 2 ml of tetrahydrofuran and 4 ml of tert-butanol is added over a period of 5 minutes, and then stirring is continued for 2 hours. At the end of this period the reddish-copper colored upper phase almost disappears and the lower phase is nearly colorless under stirring. Thereafter using a procedure analogous to that of Example 1, 1.0 g of crude MEE is obtained.

Gas chromatographic analysis indicated a 97.5% conversion and a 89.3% selectivity.

REFERENCE EXAMPLE 6

This reference example illustrates that when the solubility of sodium in the lower phase is low as compared with that of Reference Example 5, intensification of the stirring does not increase the conversion to a sufficient extent. Using 1.0 g of EMK, 1.0 g of sodium, 60 ml of tetrahydrofuran and 20 ml of liquid ammonia, Reference Example 5 is repeated.

Gas chromatographic analysis indicated a 89.8% conversion and a 93.6% selectivity. 

What is claimed as new and intended to be covered by Letters Patent is:
 1. In a process for producing a 17-acetal of a 3-alkoxyestra-2,5(10)-dien-17-one having the formula (I): ##STR2## wherein R₁ and R₂ when considered separately are C₁ -C₁₀ alkyl;R₁ and R₂ when taken together are C₂ -C₁₀ alkylene; and R₃ is C₁ -C₁₀ alkyl; which comprises reacting a 17-acetal of a 3-alkoxyestra-1,3,5(10)-trien-17-one having the formula (II): ##STR3## wherein R₁, R₂ and R₃ are as defined herein above, with sodium or potassium, liquid ammonia and a tertiary alcohol in the presence of a solvent selected from the group consisting of tetrahydrofuran, dioxane and tetrahydropyran, the improvement which comprises: conducting said reaction with not more than 90 ml (measured at the boiling point of the system) of liquid ammonia per gram of sodium or potassium, not more than 100 ml (measured at 15° C) of said solvent per gram of sodium or potassium, said sodium or potassium and said 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one being present in such proportions that said 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one is substantially dissolved in the reaction system and that two liquid phases are formed in the reaction system, the upper phase of which consists essentially of sodium or potassium and liquid ammonia and the colored lower phase consisting mainly of said solvent, liquid ammonia and said 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one.
 2. The process of claim 1, wherein the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one is 3-methoxyestra-1,3,5(10)-trien-17-one ethylene acetal.
 3. The process of claim 1, wherein the solvent is tetrahydrofuran.
 4. The process of claim 1, wherein the tertiary alcohol is tert-butyl alcohol or tert-amyl alcohol.
 5. The process of claim 4, wherein the tertiary alcohol is tert-butyl alcohol.
 6. The process of claim 1, wherein sodium is the reducing agent.
 7. The process of claim 1, wherein the components of said reaction are 3-methoxyestra-1,3,5(10)-trien-17-one ethylene acetal, liquid ammonia, tetrahydrofuran and sodium.
 8. The process of claim 1, wherein said reaction system contains no more than 75 ml of liquid ammonia per gram of sodium or potassium, and no more than 75 ml of the solvent per gram of sodium or potassium.
 9. The process of claim 8, wherein said reaction system contains no more than 60 ml of liquid ammonia per gram of sodium or potassium, and no more than 60 ml of the solvent per gram of sodium or potassium.
 10. The process of claim 1, wherein said reaction system contains at least 2 gram equivalents of sodium or potassium per mole of the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one.
 11. The process of claim 10, wherein said reaction system contains 3.0 to 10 gram equivalents of sodium or potassium per mole of the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one.
 12. The process of claim 1, wherein the tertiary alcohol is provided in an amount sufficient to give 2 equivalents of proton per mole of the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one.
 13. The process of claim 1, wherein the tertiary alcohol is provided in an amount to yield from 2 to 4 equivalents of proton per mole of the 17-acetal of the 3-alkoxyestra-1,3,5(10)-trien-17-one.
 14. The process of claim 1, wherein the tertiary alcohol is added 0.5 to 2 hours after the initiation of the reaction. 